A dynamic optimization control approach of life cycle energy saving for heat exchanger network with bypasses

被引:0
作者
机构
[1] Research Institute of Automation, China University of Petroleum
[2] Department of Chemical and Biological Engineering, University of British Columbia, Vancouver
来源
Luo, X. (luoxl@cup.edu.cn) | 1600年 / Materials China卷 / 64期
关键词
Bypass; Energy saving; Heat exchanger network; Life cycle; Optimization control;
D O I
10.3969/j.issn.0438-1157.2013.04.030
中图分类号
学科分类号
摘要
In order to achieve sustainable energy saving of heat exchanger network in the life cycle, bypasses were set in the network to increase its control degree of freedom, while a certain margin was designed to provide operating space of optimal control. To better use bypass adjustment and margin of operating space, an optimal control approach method based on dynamic model of heat exchanger network was presented and combined with existing conventional control loop, not only expanding the feasible region of optimal control, but also meeting the accuracy requirements of the original conventional control loop. The cumulative cost minimization of heat exchanger network within a certain period was considered as the objective function, while considering the impact of disturbances on heat exchanger network. To meet the process conditions, the best bypass opening in the life cycle was solved in order to achieve sustained energy saving of heat exchanger network. Closed-loop correction, iterative and rolling implementation were adopted, and optimization was based on actual conditions. A global sub-optimal solution could only be arrived at every turn. However, the actual control result could achieve the optimum. Finally, a refinery's crude oil heat exchanger network was treated as the specific study object, illustrating the effectiveness and application prospect of the presented method. © All Rights Reserved.
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页码:1340 / 1350
页数:10
相关论文
共 19 条
[1]  
Zheng S., Further decreasing the energy consumption of petroleum refining enterprises, Petroleum Refinery Engineering, 33, 8, pp. 50-54, (2003)
[2]  
Meng X., A review of energy saving in China's refining industry, Petrochemical Industry Trends, 13, 3, pp. 31-35, (2005)
[3]  
Jiang L., Feng X., Ding S., Analysis of retrofitting the process controlled by network pinch, Journal of Chemical Engineering of Chinese Universities, 15, 2, pp. 161-166, (2001)
[4]  
Fan X., Wang S., Kuang G., Et al., Energy analysis in process system, Chemical Fertilizer Design, 136, 60, pp. 11-16, (1998)
[5]  
Calandranis J., Stephanopoulos G., Structural operability analysis of heat exchanger networks, Chemical Engineering Research and Design, 6, 9, pp. 347-364, (1986)
[6]  
Jezowski J., Bochenek R., Jezowski A., Pinch locations at heat capacity flow-rate disturbance of streams for minimum utility cost heat exchanger networks, Applied Thermal Engineering, 20, 15, pp. 1481-1494, (2000)
[7]  
Westphalen D.L., Young B.R., Svrcek W.Y., Strategies for the operation of heat exchanger networks based on structural information, Computers & Chemical Engineering, 20, pp. 823-829, (1996)
[8]  
Ni J., Cui G., Jiang H., Hu X., Flexibility identification and operation optimization based on by-pass adjustment of heat exchanger networks, Chemical Industry and Engineering Progress, 29, 1, pp. 17-24, (2010)
[9]  
Boyaci C., Uzturk D., Konukman A.E.S., Et al., Dynamics and optimal control of flexible heat-exchanger networks, Computers & Chemical Engineering, 20, pp. 775-780, (1996)
[10]  
Luo X., Sun L., Zhang J., Optimal design of bypass location on heat exchanger networks, Journal of Chemical Industry and Engineering(China), 59, 3, pp. 646-652, (2008)